EP2610568A1 - Trockenverfahren für eine Beschichtung - Google Patents

Trockenverfahren für eine Beschichtung Download PDF

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Publication number
EP2610568A1
EP2610568A1 EP13001367.5A EP13001367A EP2610568A1 EP 2610568 A1 EP2610568 A1 EP 2610568A1 EP 13001367 A EP13001367 A EP 13001367A EP 2610568 A1 EP2610568 A1 EP 2610568A1
Authority
EP
European Patent Office
Prior art keywords
drying
coating
coating layer
web
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP13001367.5A
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English (en)
French (fr)
Inventor
Kazuhiro Oki
Takeshi Kitaoka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujifilm Corp
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Fujifilm Corp
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Filing date
Publication date
Priority claimed from JP2003084846A external-priority patent/JP4004429B2/ja
Priority claimed from JP2003084847A external-priority patent/JP4601909B2/ja
Application filed by Fujifilm Corp filed Critical Fujifilm Corp
Publication of EP2610568A1 publication Critical patent/EP2610568A1/de
Withdrawn legal-status Critical Current

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
    • F26B13/14—Rollers, drums, cylinders; Arrangement of drives, supports, bearings, cleaning
    • F26B13/18—Rollers, drums, cylinders; Arrangement of drives, supports, bearings, cleaning heated or cooled, e.g. from inside, the material being dried on the outside surface by conduction
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10—Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/005—Treatment of dryer exhaust gases
    • F26B25/006—Separating volatiles, e.g. recovering solvents from dryer exhaust gases

Definitions

  • the present invention relates to a drying method and a drying apparatus for drying a coating layer, and particularly to a drying method and a drying apparatus for drying a coating layer on a continuous and wide coating surface of a web as a continuously running flexible substrate while at least one liquid composition is applied on the web so as to form the coating layer.
  • an wind is blown from an air nozzle to dry a wet coating layer on a coating surface of the web while another non-coating surface of the web is supported by rollers, and otherwise an wind is blown from an air nozzle to both coated and non-coating surfaces of the web to float the web in the atmosphere and to simultaneously dry the coating layer on the web in a situation in which the web is not supported by the rollers.
  • the latter one is a non-contact type.
  • S48-042903 discloses another non-contact type of a method and an apparatus for drying the wet coating layer, in which a web is coiled on a surface of a cylindrical dryer and an air is blown through holes formed on a wall of the cylindrical dryer. Thus the dry is effectively performed.
  • blow-drying method Such method and apparatus for drying the wet coating layer with blowing the heated air is called a blow-drying method and a blow-drying apparatus in below.
  • the blow-drying method the moisture of the wind is usually adjusted, and thereafter the wind is blown onto the coating surface so as to evaporate the solvent and to dry the coating layer on the coating surface.
  • the blow-drying method is excellent in the drying efficiency, the wind is blown to the coating layer directly or through a porous plate, straightening plate, or the like, which causes the bad conditions for the coating layer. Accordingly, the thickness of the coating layer loses uniformity, and unevenness or mura is generated. Further, the convection of the wind makes the evaporation speed of the solvent from the coating layer on coating surface nonuniform.
  • the coating surface of the web has the orange peel of the coating layer ( Ozaki, Yuji "Coating Technology" Asakura-shoten, 1971, Page 293-294 ). Accordingly, it is hard to form the coating layer having the uniform thickness.
  • the unevenness is generated so much.
  • the reason therefor is as follows: in the primal situation, the organic solvent is contained enough, and when the organic solvent evaporates in this situation, the coating layer has the temperature distribution and a surface tension distribution. In this case, the marangoni convection occurs to generate the unenvenness in the coating layer. The generation of the unevenness is a considerable coating defect. Further, when the liquid crystal compounds are contained in the coating layer, it is hard to obtain the predetermined and uniform orientation by blowing the wind to the substrate.
  • the Japanese Patent Laid-Open Publication No. 2001-170547 (Page 3-5, Fig.1 ) teaches a drying method in which a drying apparatus is disposed just after the coating process.
  • the drying space in the drying apparatus is separated into plural chambers. In each chamber, a wind is blown in a widthwise from a side to another side of the web while the wind-velocity is controlled. Thus the generation of the unevenness is reduced.
  • the Japanese Patent Laid-Open Publication No. H09-073016 (Page 5, FIG.5 ) discloses a drying method in which wire-nettings are provided for the same purpose instead of separating the drying space of the drying apparatus.
  • the concentration of the coating solution becomes higher or the thickener is added to the coating solution to make the viscosity higher, so as to reduce the convection of the coating layer in blowing the wind just after the coating process.
  • the leveling effect also reduces the generation of the unevenness when the convection of the coating layer occurs in the wind blown to the coating layer just after the coating process.
  • the above two methods are not adequate for the high speed coating, and increase the drying time, which causes the extremely low productivity.
  • Japanese Patent Laid-Open Publication No. 2000-157923 (Page 2-3, FIG.1 ) teaches a drying method in which the wind velocity is controlled so as to be lower.
  • Great Britain Patent 1401041 and United States Patents 5168639 , 5694701 disclose a drying method in which no wind is blown.
  • the solvent in the coating layer evaporates without wind to perform the drying, and the generated vapor gas is recovered.
  • an entrance and an exit of the substrate is provided in an upper side of a casing of the drying apparatus.
  • a non-coating surface of the substrate is heated to promote the evaporation of the solvent from the coating surface for performing the dry.
  • a solvent vapor is generated, and condensed with a condenser which is disposed in a side of the coating surface, so as to dry the coating layer.
  • a drum is disposed above the horizontally running substrate so as to recover the solvent vapor.
  • United States Patent 5694701 proposes a drying method as an improvement of a layout of United States Patent 5168639 .
  • the coating surface of the substrate is directed upward, and the substrate is fed in a almost horizontal direction.
  • the solvent vapor easily escapes in a widthwise direction of the web, which causes the generation of the unevenness.
  • a medium having a high temperature such as a hot water, is used for heating the non-coating surface of the substrate.
  • the medium of the high temperature contacts to or is closed to the substrate, the coating surface of the substrate becomes extremely high, which is preferable in view of promotion of drying.
  • the solvent evaporates at a high speed.
  • the coating layer is often not uniformly dried, or the high temperature decreases the viscosity of the coating layer on the substrate such that the streaming of the solution occurs in the coating layer.
  • the heating means is not used, the temperature of the coating layer becomes lower by the evaporation of the solvent. Accordingly, the drying speed becomes extremely lower, and plashing occurs in the latter half of the dryer.
  • An object of the present invention is to provide a drying method and a drying apparatus for a coating layer on a coating surface of a substrate effectively and with reducing the generation of the unevenness, while at least one liquid composition is cast to form the coating layer on the substrate.
  • a drying method for drying a coating layer which is formed by coating a moving web with a coating solution the web is transported almost vertically and upward immediately after the coating.
  • the transporting direction of the web is inclined with one or larger number of guide rollers from an almost vertical direction toward a horizontal direction gradually.
  • the coating layer is dried with a drying device having a casing which surrounds the web just after the coating while disturbance of wind close to a coating surface is prevented and concentration of the solvent vapor in a side of a surface of the coating layer is kept high.
  • a drying apparatus for drying a coating layer of the present invention includes one or more number of guide rollers for gradually including the upwardly transported web just after the coating from an almost vertical direction toward a horizontal direction. Further the drying apparatus has a casing for surrounding the web just after the coating, such that disturbance of wind close to a coating surface may be prevented, and a concentration of the solvent vapor in a side of a surface of the coating layer may be kept high.
  • the web surrounded by a casing at a transporting position is dried just after the coating with a drying device, so as to prevent disturbance of wind closed to a coating surface.
  • the heating is made with a heating means, such that a temperature difference
  • a preferable embodiment of a drying apparatus of the present invention included a drying device and a heating means.
  • the drying device is disposed at a transporting position just after the coating, while a casing surrounds the web so as to prevent disturbance of wind closed to a coating surface.
  • the heating means is disposed within the drying device for controlling a temperature difference
  • the drying device is disposed at a transporting position just after the coating while a casing surrounds the web so as to prevent disturbance of wind closed to a coating surface.
  • a heating means is disposed within the drying device for controlling a temperature difference
  • the wide coating layer continuously formed on a coating surface of the substrate by casting the coating solution is uniformly and effectively dried since the generation of the unevenness just after the application of the coating layer is restrained.
  • the layout of the coating and drying processes does not vary so much, and the physical properties and the sorts of the coating solution are not restricted. Accordingly, the coating solution can be prepared in several methods. Furthermore, the reduction of the energy used in the production and that of the cost is effectively made. Further, in the present invention the network structure of the polymer and the particles that is formed in drying the coating layer.
  • the coating solution contains preferably at least 50% by mass.
  • the effect of the present invention is very effective, when the organic solvent is contained in the coating solution, otherwise when only one or more organic solvent is used as a solvent of the coating solution. Furthermore, the effect of the present invention is more effective, when the boiling point of the organic solvent is low.
  • a coating/drying line 10 has a feeding apparatus 12, a back-up roller 13, an extrusion die 14, a drying apparatus 16, rollers 17-19, and a winding apparatus 21.
  • the feeding apparatus 12 unwinds and feeds a web 11 wound in a web roll.
  • the back-up roller 13 confront to the extrusion die 14, such that they construct a coating apparatus for coating the web 11 with a coating solution.
  • the drying apparatus 16 dries a coating layer 15 formed of the coating solution cast on the web 11.
  • the rollers 17-19 are arranged on a transport path in which the web 11 coated with the coating solution is transported.
  • the winding apparatus 21 winds as a film product 20 produced through the coating and the drying.
  • the drying apparatus 16 includes a first guide roller 22 and a second guide roller 23.
  • the first and second guide rollers 22, 23 transport the web 11 with inclination at a transport angle (or an entrance angle) ⁇ 1 of the web to a horizontal direction in upstream from the roller 17, a transport angle ⁇ 2 of the web to a horizontal direction between the rollers 17 and 18, and a transport angle (or an exit angle) ⁇ 3 of the web to a horizontal direction between the rollers 18 and 19.
  • a wind meter 24 is provided for the drying apparatus 16, and measures the wind velocity of a wind blown in the drying apparatus 16.
  • the drying apparatus is tightly-closed such that the wind velocity is at most 0.1 m/s when the web 11 is not transported in the drying apparatus 16.
  • the drying apparatus 16 has a box-shaped heater 25 so as to have a predetermined temperature.
  • a blow-drying apparatus 26 is disposed in the coating/drying line 10. Note that the number of the guide roller is not restricted in the figure, and may be one or more.
  • the coating solution contains, for example, a discotic liquid crystal in order to produce an optical compensation sheet, otherwise a silver halide particles used for heat developing photosensitive material, and the like.
  • the coating solution is not restricted in them.
  • the composition of the organic solvent in the coating solution is at least 50 wt.%.
  • the organic solvent means an organic liquid compound with dissolubility of material.
  • the organic solvent there are aromatic hydrocarbons (toluene, xylene, styrene and the like), aromatic hydrocarbon chloride (chlorobenzene, o-dichlorobenzene, and the like), derivatives of methane (monochloromethane and the like), aliphatic hydrocarbon chloride including derivatives of ethane (monochloroethane and the like), alcohols (methanol, isoproryl alcohol, isobutyl alcohol and the like), esters (methyl acetate, ethyl acetate and the like), ethers (ethylether, 1,4-dioxane and the like), ketones (acetone, methylethylketone and the like), glycolether (ethyleneglycol monomethylether and the like), alycyclic hydrocarbon (cyclohexane and the like), aliphatic hydrocarbon (n-hexane and the
  • the other than the extrusion die 14 in FIG.1 may be used.
  • the other than the extrusion die 14 in FIG.1 may be used.
  • the coating apparatus there are a slot-die coater, a wire bar coater, a roll coater, a gravure coater, a slide coater, curtain coater, and the like. Note that when the coating is made, the surface to be coated may be directed upward or downward, and otherwise inclined to the horizontal direction.
  • a dust removing apparatus (not shown) may be provided before and after the coating apparatus.
  • the surface of the web 11 may be pretreatment.
  • An optical film preferably have high quality, for example does almost not have dust. Accordingly, when both of the provide of the dust removing apparatus and the previous processing are simultaneously adopted, then the coating and the drying of the coating layer is made with high quality.
  • the positional relation between the back-up roller and the first or second guide roller 22, 23 is determined such that the transport angle between the web transporting direction and the horizontal direction may be gradually smaller.
  • the first guide roller 22 is disposed such that the web 11 may be transported almost perpendicularly after the back-up roller 13.
  • the transport angles ⁇ 1 at an entrance, ⁇ 2 in a casing 16a, and ⁇ 3 at an exit of the drying apparatus 16 satisfy following conditions; 60 ⁇ ° ⁇ ⁇ ⁇ 3 ⁇ ⁇ ⁇ 2 ⁇ ⁇ ⁇ 1 ⁇ 90 ⁇ ° , ⁇ ⁇ 3 ⁇ ⁇ ⁇ 1.
  • the transporting direction is directed upward at in the range of 60°-90°, and the coating surface is disposed in upper side.
  • the transporting direction is particularly preferably 75°-89°, especially preferably 75°-88° .
  • the transporting direction is less than 60°, then a speed at which the solvent vapor flows down in the effect of the gravity becomes smaller, and the solvent vapor easily escapes from the side of the coating layer. Therefore it is difficult to keep the concentration of the solvent vapor close to the coating layer high. Further, when the solvent vapor easily escapes from the side of the coating layer, the uniform concentration of the solvent vapor is lost, which causes the drying unevenness.
  • the velocity of wind in the drying apparatus is at most 0.1m/s in the situation that the web is not transported.
  • the distance L1 between the coating position and the first guide roller 22 is preferably at most 2 m, and the distance L2 between the first guide rollers 22 and 23 is preferably at most 2 m.
  • the number of the guide roller in the drying apparatus 16 is not restricted in two, but may be larger. In this case, the distance between the neighboring guide rollers is at most 2m. Further, only one guide roller may be used in the present invention.
  • the natural convection occurs in the coating solution in the coating layer 15 just after the coating on the web 11, and thus the unevenness is formed in the coating layer 15.
  • the casing 16a of the drying apparatus 16 surrounds a transport path of the web 11 after the application of the coating solution so as to prevent the disorder of the flow of the wind near to the coating surface of the web 11.
  • high concentration of a solvent vapor of the organic solvent is kept in an atmosphere in a side of the coating surface while the coating layer 15 is dried. Accordingly, the evaporation is not made suddenly, and the deformation of the web 11 and the coating layer 15 is prevented.
  • a distance L3 between the coating apparatus and an entrance of the drying apparatus 16 is preferably at most 2m, and especially at most 0.7 m.
  • the drying apparatus 16 the drying of the coating layer 15 is promoted, and thereafter the roller 17 supports the web 11 and feeds it into the blow-drying apparatus 26.
  • the roller 17 may be a free roller, or a drive roller to which a driving device (not shown) is attached.
  • the length of the casing 16a can be determined independent of the transport conditions.
  • a jacket is attached to each guide roller 22, 23 so as to obtain a jacket roller for controlling the temperature.
  • the coating layer 15 is further dried, and thus the film product 20 is obtained from the web 15.
  • the dryer of the prior art such as a roller transport type, a floating type, a coil-type, and the like.
  • the non-coating surface is supported by rollers, and a wind is blown from a air nozzle to the coating surface.
  • a wind is blown from a air nozzle to both coated and non-coating surfaces of the web to float the web in the atmosphere and to simultaneously dry the coating layer on the web in a situation in which the web is not supported by the rollers.
  • a coil type drying apparatus is used so as to use a space effectively and make the drying effectively. In these dryers, there is a common point that the dry wind is supplied to the coating surface of the web 11.
  • rollers 18, 19 are also the free roller or the drive roller as the roller 17.
  • the extrusion die 14 casts a coating solution to form a coating layer 41 on the web 11.
  • a drying apparatus 42 includes condensers 43-45 and box-shaped heaters 46-48 in another side from the web 11. Further, a side of the coating layer 41 is separated with a partation plates 51, 52 to form a first space 42a between a first guide roller 49 and a entrance of the drying apparatus 42, a second space 42b between a second guide roller 50 and the first guide roller 49, and a third space 42c between an exit of the drying apparatus 42 and the second guide roller 50.
  • the first-third spaces 42a-42c are respectively provided with the condensers 43-45.
  • the heaters 46-48 simultaneously promote to evaporate from the coating layer a solvent containing the organic solvent under control.
  • the heaters 46-48 are disposed in a side of the non-coating surface of the web 11 and respectively opposite to the condensers 43-45.
  • a feed roller (heating roller) whose temperature is made higher may also be provided in the heating apparatus 40.
  • an infrared ray heater and a microwave heating means may be used to heat the web 11.
  • the infrared ray heater is preferably radiates low infrared ray, and has, for example, a box-like shape whose surface is flat and jackets in which a how water flows. In this case, the setting distance between the web 11 and the infrared ray heater and the temperature are regulated accurately. Accordingly, a drying temperature for drying the coating layer can be controlled precisely.
  • the condensers 43-45 are disposed with a predetermined distance from the web 11, and have plate shapes so as to be parallel to the feeding direction of the web 11. Coolers 53-55 of a heat exchanger type are respectively connected to and feed cooling medium 56 into the condensers 43-45.
  • the condensers 43-45 condense and recover the evaporated organic solvent.
  • the materials used for the condensers 43-45 may be metal, plastics, wood and the like. However, they are not restricted especially. When the organic solvent is contained in the coating solution, it is preferable to use the material having a resistance to the organic solvent or to make the coating on the surface of the condenser.
  • the regulation of the temperatures of each condenser 43-45 is preferably made.
  • the drying speed of the coating layer 41 is controlled.
  • the condenser 43 As shown in FIG. 3 , on a condensing surface of the condenser 43 are formed protrusions 43a and grooves 43b so as to extend in a lengthwise direction, and the condenser 43 is disposed such that the lengthwise direction may be the transporting direction. Accordingly, in the effect of the gravity, the condensed solvent flows downwards in the grooves 43b.
  • the condenser 43 has a gutter 43c in lower and right side of this figure for recovering the organic solvent.
  • the condenser 43 has a form or a structure not so as to generate the unnecessary forces against the gravity for the condensed solvent flowing down.
  • the condenser may have a structure so as to have the same functions as described above.
  • the condenser may be, for example, porous plates, a net, a duckboard, a roller and the like.
  • a recovering device disclosed in US Patent No.5694701 may be used simultaneously.
  • the condensers 43-45 are used, however, as shown in FIG.2B , instead of the condensers 43-45, a flow straightening plate 143-145 may be disposed parallel to the transporting direction. In this case, the coolers 53-55 in FIG.2A are not provided. Further the flow straightening plates 143-145 are made of metal, plastic, woods and the like.
  • a distance L4 between a surface 41a of the coating layer 41 and the protrusion 43a is adequately determined in consideration with the predetermined drying speed of the coating layer 41.
  • the distance L4 is shorter, then the drying speed becomes not only higher, but also the difference of the distance L4 from the predetermined value has large influence on the drying speed. Further in this case, the provability of the contact of the surface 41a to the protrusion 43a becomes larger. Otherwise, when the distance L4 is large, the drying speed does not become only much lower, but the thermal energy causes the natural convection of the coating solution to form the drying nonuniformity.
  • the distance L4 is preferably in the range of 5 mm to 10 mm.
  • the condenser 43 has a flow space 43d (see FIG. 4 ) in which the cooling medium 56 flows, and therefore the temperature is easily controlled so as to effectively recover the solvent.
  • a cooling medium such as water
  • an air cooling type in which air is used
  • electric types in which such as a peltier element is used, and the like.
  • the drying apparatus may have side plates instead of the casing. Thus it is prevented that the solvent vapor of the organic solvent diffuses from the area near to the coating surface of the web. Note that the present invention is not especially restricted when a side of the drying apparatus is tightly closed.
  • the web 11 is preferably transported at the transport speed at which the web 11 reaches the drying apparatus in three seconds from the application of the coating solution on the web 11.
  • the coating amount of the coating solution and the thickness of the coating layer are large, then the convection usually occurs easily, and therefore the unevenness is formed.
  • the coating amount of the coating solution and the thickness of the coating layer are large, the enough effect is obtained.
  • the thickness of the wet coating layer is 0.001 mm to 0.05 mm (1 ⁇ m to 50 ⁇ m)
  • the coating layer can be dried without generation of the unevenness. Note that the thickness determined as the total thickness of the coating layer formed on the web by coating the coating solution.
  • the unevenness in the coating layer is easily formed especially in early dry period during which much solvent remains in the coating layer, it is preferable that at least 70 % by mass of the solvent in the coating solution is evaporated, and condensed or reduced in the drying apparatus 16. In this case, the remaining solvent in the coating solution is evaporated in the blow-drying apparatus 26. What percentage by mass of the solvent is evaporated, it is determined in total consideration of the influence on reducing the generation of the drying nonuniformity in the coating layer, the productivity, and the like. Further, when the transport speed is too high, then the atmosphere closed to the web 11 is moved to be an unexpected wind, and the unexpected wind has a bad influence on the coating layer 15 on the web 11. Accordingly the transport speed of the web 11 is from 1 m/min to 100 m/min.
  • the web 11 in order to promote the evaporation of the organic solvent in the coating layer 15 and the condensation thereof, the web 11 is cooled in the side of the coating layer by the condensers 43-45, and heated in another side by heaters 46-48.
  • the temperatures of the web 11, the coating layer 15 and the condensers 43-45 are determined that the solvent vapor is not condensed on other parts than the condensers, for example, on surfaces of the guide roller 22, 23.
  • the temperatures of the other parts are set to be higher than those of the condensers.
  • a device or a member for thermo-insulating is provided for preventing the condensation on the gutters, and may be, for example, a device of heat-exchanging type in which water is used, a thermal insulator and the like.
  • the coating/drying line has the drying apparatus in which the drying method of the present invention is applied, the feeding apparatus, the guide rollers, the winding apparatus and the like that are provided in the coating/drying line are constructed of members which are usually used. The explanation of them is omitted.
  • the generation of the unevenness in the coating layer 15 just after the coating is prevented, and the uniform drying of the coating layer is made. Further, the layout of the drying processes is not changed too much in the present invention. Furthermore, as there is no restriction in the physical property of the coating layer and the sorts of the solvents, the preparation of the coating solution is flexibly designed.
  • the above embodiments which has a structure for condensing and recovering the solvent vapor is preferably used in the present invention.
  • the drying apparatus of the present invention is disposed between the coating apparatus and the blow-drying apparatus.
  • the casing is provided to surround the web just after the coating, such that the unexpected wind closed to the coating surface of is not generated there and the concentration of the solvent vapor is high in the side of the coating surface.
  • the effect of the present invention is obtained, and therefore the improvement of the casting/drying line is made at low cost.
  • the drying method and the drying apparatus of the present invention has the same effects when the coating solution is a solution or a dispersion of solid materials (for example the polymer or particle).
  • the particles are used as the solid material for the coating solution, the generation of the unevenness has a large influence on the dispersion state. Accordingly the present invention is applied to this case.
  • the present invention is adequately applied to the production of an optical function sheet (optical compensation sheet and the like), a prime layer formed of a photosensitive material, a heat-developable photosensitive material (or a photo film), a functional film containing micro particles (such as nanoparticles), a prime layer formed from a solvent of the film which is used as the photosensitive material, a photo film, a photographic paper, magnetic recording tape, adhesive tape, pressure sensitive paper, off-set plate material, battery, and the like.
  • a coating/drying line 60 is provided with a drying apparatus 66.
  • the same members and parts have the same numbers as in FIG.2 , and the explanation thereof is omitted.
  • the blow-drying apparatus can be used as the heat-ripening means.
  • the drying apparatus 66 includes box-shaped heaters 70-72, and thermometers 64, 65 are respectively attached to an entrance and an exit for measuring an entrance temperature T1 and an exit temperature T2 of the coating layer 15 on the web 11. Further, a thermosensor 76 is provided in the drying apparatus 66 for measuring the drying temperature T3 at the optional position of the coating layer 15 in the casing 66a. Note that the thermometers 64, 65 and the thermosensor 76 used in the coating/drying line 60 may be already known.
  • the heaters 70-72 heat the web 11 to evaporate the solvent contained in the coating layer 15.
  • condensers 73-75 disposed with a predetermined distance from the web 11 so as to be nearly parallel to the feeding direction of the web 11.
  • the condenser may have a function of a baffle plate and the like.
  • the materials used for the condenser or the plate member may be metal, plastics, wood and the like. However, they are not restricted especially.
  • the used material preferably have a resistance to the organic solvent or a character of making the coating on the surface of the plate member.
  • Coolers 53-55 are combined to the condensers 73-75, and may be, for example, a heat exchanger type for cyclically feeding a cooling medium 56, an air cooling type in which air is used, electric types in which such as a peltier element is used, and the like.
  • the drying speed of the coating layer15 is regulated, and therefore the condensing speed in condensing the solvent vapor is controlled. Accordingly, during the dry of the coating layer, the concentration of the solvent vapor in the atmosphere between the coating layer 15 and the condenser 73-75 can be easily kept to be high. In this situation, the drying of the coating layer 15 is not suddenly made, and therefore the deformation of the coating layer and the web, (or the generation of the unevenness) is prevented.
  • the drying apparatus may be provided with parts which have the same functions, for example, porous plates, a net, a duckboard, a roller and the like. Further, a recovering device disclosed in US Patent No.5694701 may be used simultaneously.
  • the condensing surfaces 73a-75a are provided with protrusions and recesses (not shown) so as to form grooves (not shown) extending in web transporting direction.
  • the condensed solvent flows in the grooves and therefore the recovery of the condensed solvent is made smoothly.
  • the condensers 73-75 are provided with gutters 73b-75b so as to remove the condensed solvent from the condensing surfaces 73a-75a of the condensers 73-75.
  • the temperatures of the web 11, the coating layer 15 and the condensers 73-75 are determined than the solvent vapor is not condensed on other parts than the condensers, for example, on surfaces of the guide rollers 49, 50.
  • the temperatures of the other parts are set to be higher than those of the condensers.
  • the drying apparatus 66 has the casing 66a which surrounds the web and tightly closes the inside except the entrance and the exit such that the atmosphere in or out of the casing 66a is fed out or sucked in the drying apparatus 66. Further, just after the application of the coating solution, the generation of the unevenness in the natural convection of the coating layer is prevented.
  • the drying apparatus is disposed just after the coating process. Concretely, the distance D1 between the coating position and the entrance of the drying apparatus 66 is preferably at most 2m, and especially preferably at most 0.7m.
  • the web 11 is preferably transported at the transport speed at which the web 11 reaches the drying apparatus 66 in three seconds from the application of the coating solution on the web 11.
  • the coating amount of the coating solution and the thickness of the coating layer are large, then the convection usually occurs easily, and therefore the unevenness is formed.
  • the coating amount of the coating solution and the thickness of the coating layer are large, the enough effect is obtained.
  • the thickness of the wet coating layer is 0.001 mm to 0.05 mm (1 ⁇ m to 50 ⁇ m)
  • the coating layer can be dried without generation of the unevenness. Note that the thickness determined as the total thickness of the coating layer formed on the web by coating the coating solution.
  • the transport speed of the web 11 is from 1 m/min to 100 m/min.
  • the unevenness in the coating layer is easily formed especially in early dry period in which the content of the solvent in the coating layer is large, it is preferable that at least 70 % by mass of the solvent in the coating solution is evaporated, and condensed or reduced in the drying apparatus 66. In this case, the remaining solvent in the coating solution is evaporated in the blow-drying apparatus 26. What percentage by mass of the solvent is evaporated, it is determined in total consideration of the influence on the coating layer for the generation of the unevenness, the productivity, and the like.
  • the entrance temperature T1 at the entrance of the drying apparatus 66 and the exit temperature T2 of the coating layer 15 at the exit are respectively controlled such that the difference (
  • the drying temperature of the coating layer 15 in the casing 66a of drying apparatus 66 is determined as the drying temperature T3
  • ) between the inside and the entrance of the drying apparatus 66 is at most 5°C.
  • the control of the temperatures at the entrance, the inside and the exit are independently made between the heaters 70-72.
  • the shape and the number of the heaters provided for the drying apparatus 66 is not restricted in the figure.
  • the three heaters are separately provided in the figure.
  • only one heater may be provided in the drying apparatus.
  • the temperatures are controlled at plural parts of the one dryer. The control of each temperature is made on the basis of the data monitored by the thermometers 64, 65 at the entrance and the exit, and the thermosensor 76.
  • a straitening plate may be provided instead of the condensers similar to the structure in FIG.2B .
  • a distance D2 between the condensing surface 73a and the coating surface of the web 11 is, in order to reduce the generation of the unevenness, set adequately in consideration of the predetermined drying speed of the coating layer 15.
  • the preset distance D2 is small, the drying speed becomes higher.
  • the difference of the preset distance D2 from the predetermined value has large influence on the drying speed. In this'case, the provability of the contact of the surface of the coating layer 15 to the condensing surface 73 becomes larger.
  • the preset distance D2 is preferably in the range of 5 mm to 10 mm.
  • the condensers 74, 75 have the same structure as the condenser 73.
  • the heater 70 an infrared ray heater, and the like can be used.
  • the heater 70 is the infrared ray heater which irradiates low infrared ray in low energy range.
  • the heater 70 includes a box-like shaped heater body 81 whose surface is flat and a jacket 82 covering the heater body 81.
  • a heating medium for example hot water
  • the preset distance D3 between the web 11 and the heater (or the infrared ray heater) 70 is adequately set and the temperature of the heating medium 83 in the jacket 82 is accurately controlled by a temperature controller 84.
  • the temperature for the coating layer in the drying can be controlled precisely.
  • the present invention is not restricted in them.
  • the other heaters 71, 72 have the same structure as the heater 70.
  • a microwave heating means may be used to heat the web 11.
  • Heating rollers 90 in FIG.7 may be used instead of the guide rollers 49, 50 (in FIG.5 ).
  • the temperature of the heating rollers 90 can be controlled so as to be higher, and thus the drying of the coating layer 15 is made.
  • the heating roller 90 has a medium chamber 91, and is connected through a pump 93 to a heater 94.
  • the heater 94 supplies a thermal energy to a heating medium 92 so as to regulate the temperature of the heating medium 92 to the predetermined value.
  • the pump 93 is driven, then a heating medium is cyclically fed between the heater 94 and the medium chamber 91 of the heating roller 90.
  • the length of the casing 66a can be determined independent from the restriction of the transport.
  • the guide rollers 49, 50 are heated with the heaters 70-72 to have the higher temperature, it is preferable that a jacket is used as each guide roller 49, 50, so as to control the temperature.
  • the drying apparatus is not restricted in the above description. While the coating/drying line has the drying apparatus in which the drying method of the present invention is applied, the feeding apparatus, the guide rollers, the winding apparatus and the like that are provided in the coating/drying line are constructed of members which are usually used. However, the explanations of them are omitted.
  • the optical compensation film is produced in the film production line.
  • the drying apparatus of FIG. 2 that has the casing to surround the web after coating is disposed, so as to prevent the unexpected flow of air near to the coating layer.
  • the estimations of the optical compensation films as film products are made while the angle between the web transporting direction at the entrance and at the exit is varied.
  • Processes for producing the optical compensation film in the film production line are as follows:
  • Example 1 of the film production method of the optical compensation sheet the processing is sequentially carried out from the feeding process of the continuous transparent film to winding process of the obtained optical compensation sheet.
  • a 5 wt.% solution of long chain alkyl modified Poval MP-203, produced by Kuraray Co. LTD.: "Poval” is a trade name
  • MP-203 long chain alkyl modified Poval
  • the transporting velocity of the continuous film is 20 m/min.
  • nx and ny are determined as refractive index according to two perpendicular directions in a film surface, nz as that according to a thickness direction, and d as thickness of the continuous film.
  • the formation of the polymer layer for the orientation layer is performed in a coating/drying line in which the drying apparatus of the present invention is provided.
  • the transport angle ⁇ 1 at the entrance of the drying apparatus is 90°
  • the transport angle ⁇ 3 at the exit of the drying apparatus is 84°.
  • the continuous film on which the polymer layer is formed is transported at 20m/min of transport speed, and simultaneously the surface of the polymer layer is rubbed.
  • a rubbing roller is used and rotated at 300 rpm. Thereafter, dusts are removed from the obtained orientation layer.
  • the continuous film having the orientation layer is transported at 20 m/min, and a 10 wt.% mixture solution of a mixture in methylethylketone is applied as the coating solution to the orientation layer with use of a wire bar coater as the coating apparatus.
  • the mixture is prepared as follows: discotic compounds TE-(1) and TE-(2) (see, chemical formula CH1) are mixed in a weight ratio of 4:1, and a photo initiator (IRGACURE 907, produced by Ciba Geigy Japan Limited.) is added to 1 wt.% to the mixted discotic compounds to obtain the mixture.
  • the coating speed is 20 m/min, and the coating volume is 5 cc/m 2 , and the continuous film is transported through the drying zone and the heating zone. In the drying zone, a wind is fed, and the temperature of the heating zone is adjusted to 130 ° C . After three seconds from the coating, the coated part of the continuous film enters in the drying zone, and further fed after three seconds into the heating zone.
  • the continuous film on which the liquid crystal layer and the orientation layer are formed is continuously transported at a transport speed of 20 m/min, and a UV ray (illuminance: 600 mW) is radiated on a surface of the liquid crystal layer with use of the UV ray radiating device (Power of UV lamp: 160 W/cm, wavelength of the UV ray: 1.6 m).
  • a UV ray illumination: 600 mW
  • Power of UV lamp 160 W/cm, wavelength of the UV ray: 1.6 m
  • Examples 2-4 and Comparisons 1-5 the optical compensation films are produced while the coating method and the transporting angles are varied.
  • the other conditions are the same as Example 1.
  • the estimations of the Examples 1-4 and Comparisons 1-5 are made, and the grade of the estimation is Good when the unevenness is not generated in the drying process and the quality of the coating layer is good, and Refused when the unevenness is generated in the drying process, the coating layer is not smooth, and the quality of the coating layer is wrong.
  • the coating/drying line 60 of FIG. 5 is used. Note that, when the heating devices are used in the drying apparatus 66, the temperatures at the entrance and at the exit are respectively set to 25 ° C and to 21 ° C . The transporting angles are fixed, and the drying conditions are varied between Examples 5-7 and Comparisons 6-8. Other conditions are the same as Experiment 1. The estimations of the Examples 5-7 and Comparisons 6-8 are made. Table 2 shows the drying conditions and the results of the grade of the estimations. The drying condition is: "All", three heaters are used; Part, a part of the three heaters are used; None, no heater is used.
  • Example 8 and Comparison 9 are produced in the film production line.
  • the transporting direction in the drying apparatus is set such that the non-coating surface of the substrate may be upward. Thereby, and the transporting angles are 90° and 60° in Example 8, and 15° and 0° in Comparison 9. Then Example 8 and Comparison 9 are compared with each other.
  • the coating solution to be applied to the web for heat-developable photosensitive material are as follows:
  • 22g phthalated gelatin and 30 mg KBr are dissolved to 700ml water at 35 ° C , such that pH may be 5.
  • the coating solution for forming an emulsion layer following materials or compounds with amount to one mol Ag are added to the organic materials in the following processes.
  • the emulsion of the silver salt of organic acid is stirred at 25 ° C , and to the organic acid silver emulsion are thereby added 10mg sodium phenyl thiosulfonate, 68mg coloring matter 1, 30mg coloring matter 2, 2g 2-melcapt-5-methylbenzoimidazol, 21.5g 4-chlorobenzophenone-2-carboxylic acid, 580g 2-butanon, and 220g dimethylformamide. Thereafter this mixture is left stationary for 3 hours.
  • the emulsion of the silver salt of organic acid is stirred, and to the emulsion are thereby added 8g 5-tribromomethyl sulfonyl-2-methylthiadiazol, 6g 2-tribromomethylsulfonyl benzothiazol, 5g 4,6-ditrichloromethyl-2-phenyltriadine, 2g disulfide compounds, 160g 1,1-bis(2-hydroxy-3-5-dimethylphenyl)-3,5,5-trimethylhexane, 5g tetrachlorophthalic acid, 1.1g fluoride type surfactant, 590g 2-butanone, and 10g methylisobutylketone.
  • a substrate of polyethylenetelelphthalate (PET) that has colored taste with use of a blue dye is used as the web.
  • PET polyethylenetelelphthalate
  • the substrate is coated with the coating solution for forming the emulsion layer that is prepared as described above, such that the surface density of the silver may be 2.3 g/cm 2 .
  • the transporting direction in the drying apparatus is set such that, in Example 8, the respective entrance and exit angles of the drying apparatus may be 90° and 60°, and in Comparison 9, 15° and 0°.
  • the condition of the surface of the product of Example 8 is good, and that of the Comparison 9 is bad as there are influences of the generation of the unevenness in the unexpected blow.
  • Example 9 the difference of the temperature between the entrance and the exit is set to 2° C , and in Comparison 10 the temperature to 7° C without use of the heater in the drying apparatus.
  • the coating solution to be applied to the web for heat-developable photosensitive material are as follows:
  • 22g phthalated gelatin and 30 mg KBr are dissolved to 700ml water at 35 ° C , such that pH may be 5.
  • the coating solution for forming an emulsion layer following materials or compounds with amount to one mol Ag are added to the organic materials in the following processes.
  • the emulsion of the silver salt of organic acid is stirred at 25 ° C , and to the organic acid silver emulsion are thereby added 10mg sodium phenyl thiosulfonate, 68mg coloring matter 1, 30mg coloring matter 2, 2g 2-melcapt-5-methylbenzoimidazol, 21.5g 4-chlorobenzophenone-2-carboxylic acid, 580g 2-butanon, and 220g dimethylformamide. Thereafter this mixture is left stationary for 3 hours.
  • the emulsion of the silver salt of organic acid is stirred, and to the emulsion are thereby added 8g 5-tribromomethyl sulfonyl-2-methylthiadiazol, 6g 2-tribromomethylsulfonyl benzothiazol, 5g 4,6-ditrichloromethyl-2-phenyltriadine, 2g disulfide compounds, 160g 1,1-bis(2-hydroxy-3-5-dimethylphenyl)-3,5,5-trimethylhexane, 5g tetrachlorophthalic acid, 1.1g fluoride type surfactant, 590g 2-butanone, and 10g methylisobutylketone.
  • Example 9 175 ⁇ m of a substrate of polyethylenetelelphthalate (PET) that has colored taste with use of a blue dye is used as the web.
  • the substrate is coated with the coating solution for forming the emulsion layer that is prepared as described above, such that the surface density of the silver may be 2.3 g/cm 2 .
  • the drying is made at first in the drying apparatus in which the solvent is condensed and recovered, and thereafter in the blow-drying apparatus. Thereafter the UV-ray is irradiated onto the coating surface of the substrate, and thus the heat developing photosensitive material is obtained.
  • the dryers are not used in the heating apparatus, and the gel-like film is transported in the condition of the difference of the temperature is 7, and then the drying in the blow-drying apparatus follows. Thereafter the UV-ray is irradiated onto the coating surface of the substrate, and thus the heat developing photosensitive material is obtained.
  • the present invention also refers to a drying method for drying a coating layer 41 which is formed by coating a moving web 11 with a coating solution containing organic solvent, comprising steps of:
  • one or plural guide roller 22, 49 are disposed within said drying device 16, 42, 66.
  • said transporting direction is directed upwardly with 60° - 90° inclination to a horizontal direction, and said coating surface is positioned upside.
  • velocity of said wind inside said drying device 16, 42, 66 is less than 0.1 m/s in a situation in which the transport of said web 11 is stopped.
  • said coating layer 41 is dried by a heat-drying means disposed downstream from said drying device 16, 42, 66.
  • an interval between a coating position and said first guide roller 22, 49 disposed closest to said coating position within said drying device 16, 42, 66 relative said transporting direction of said web 11 is less than 2m.
  • drying device 16, 42, 66 is disposed within 0.7m after the coating.
  • a plate-like 25 member is used for said device for condensing and recovering.
  • each said device is disposed in a space formed by partitioning an inside of said drying device 16, 42, 66 with said guide roller 22, 49 s.
  • said plate-like member is provided for a cooling apparatus, and temperature of said plate member is adjustable with use of said cooling apparatus.
  • a flow path in which said condensed organic solvent flows in effect of gravity is provided on a surface of said plate-like member.
  • side plates are disposed on both sides of said drying device 16, 42, 66, or said sides are tightly closed so as to prevent said solvent vapor from said coating layer 41 from flowing out of said both sides of said drying device 16, 42, 66.
  • a content of said organic solvent in said coating solution is at least 50% by mass.
  • said drying device 16, 42, 66 dries at least 70% by mass of said organic solvent contained in said coating solution.
  • thermoforming device in a side of a non-coating surface of a transport position of said web 11 within said drier.
  • a thickness of said wet coating layer 41 is at most 50 ⁇ m.
  • the coater is used to apply said coating solution on said web 11 supported by a back-up member.
  • At least a wire bar coater or a graver coater is used to apply said coating solution on said web 11.
  • the present invention also relates to a drying apparatus for drying a coating layer 41 which is formed by coating a moving web 11 with a coating solution containing organic solvent, comprising:
  • a blow-drying apparatus 26 is disposed downstream from said drier.
  • the present invention also refers to a drying method for drying a coating layer 41 which is formed by coating a moving web 11 with a coating solution containing organic solvent, comprising steps of; drying said web 11 surrounded by a casing 16a, 42a, 66a at a transporting position just after the coating with a drying device 16, 42, 66, so as to prevent disturbance of wind closed to a coating surface, said drying device 16, 42, 66 having a heating means; heating with said heating means, such that a temperature difference
  • said heating means heats so that a temperature difference
  • drying device 16, 42, 66 does not blow and discharge a wind.
  • said drying is made while a solvent vapor above a side of the coating surface within said drying device 16, 42, 66 is kept at high concentration in a middle of drying.
  • said coating layer 41 is dried by a blow-drying 44 apparatus 26 disposed downstream from said drying device 16, 42, 66.
  • drying device 16, 42. 66 is disposed downstream at most 0.7m after the coating.
  • a device for condensing and recovering a solvent vapor evaporated from said coating layer 41 is disposed in a side of a coating surface at a transporting position of said web 11 within said drying device 16, 42, 66.
  • a content of said organic solvent in said coating solution is at least 50% by mass.
  • drying device 16. 42, 66 dries at least 70% by mass-of said organic solvent in said coating solution.
  • an infrared ray heater 25, 46, 47, 48, 70, 71, 72 is used as said heating means.
  • a temperature of water is controlled in the range of 40°C to 80°C with use of said infrared ray heater 25, 46, 47, 48, 70, 71, 72, and said water is used as said heating means.
  • said infrared ray heater 25, 46, 47, 48. 70, 71, 72 has a box shape.
  • said infrared ray heater 25. 46. 47, 48, 70. 71, 72 is disposed 10mm to 50mm apart from said web 11.
  • a guide roller 22, 49 is disposed within said drying device 16, 42, ,66, and said guide roller 22, 49 is a roller whose temperature is controlled.
  • a thickness of said wet coating layer 41 is at most 50 ⁇ m.
  • the present invention also refers to a drying apparatus for drying a coating layer 41 which is formed by coating a moving web 11 with a coating solution containing organic solvent, comprising; a drying device 16, 42. 66 disposed at a transporting position just after the coating, while a casing 16a, 42a, 66a surrounds said web 11 so as to prevent disturbance of wind closed to a coating surface; and a heating means disposed within said drying device 16.
  • 42, 66 for controlling a temperature difference
  • the present invention refers to a drying apparatus for drying a coating layer 41 which Is formed by coating a moving web 11 with a coating solution containing organic solvent, comprising:
  • a blow-drying apparatus 26 is disposed downstream from said drying device 16, 42, 66.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Drying Of Solid Materials (AREA)
  • Coating Apparatus (AREA)
EP13001367.5A 2003-03-26 2004-03-26 Trockenverfahren für eine Beschichtung Withdrawn EP2610568A1 (de)

Applications Claiming Priority (3)

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JP2003084846A JP4004429B2 (ja) 2003-03-26 2003-03-26 塗布膜の乾燥方法および装置
JP2003084847A JP4601909B2 (ja) 2003-03-26 2003-03-26 塗布膜の乾燥方法及び装置
EP04007398.3A EP1462746B1 (de) 2003-03-26 2004-03-26 Trocknungsverfahren und Trocknungsvorrichtung für eine Beschichtung

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US8828501B1 (en) 2014-09-09
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EP1462746A2 (de) 2004-09-29
EP2610567A1 (de) 2013-07-03
US20040191419A1 (en) 2004-09-30

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